• Journal of Korean Society of Environmental Engineers
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• v.32 no.2
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• pp.131-140
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• 2010

Zero waste clean city was visualized by designing the environmental fundamental facilities such as automated waste collection and bio-energizing system of domestic waste, which was categorized into food and combustible waste from urban area. The biomass circulation position was applied to the domestic waste collection position combined with bio-energizing system in the zero waste clean city. Bio-energizing system consisted of bio-gasification, bio-fuel and bioenergy-circulation process. Food wastes were treated by bio-gasification with anaerobic digestion, and combustible wastes were made of bio-fuel with pyrolysis/drying. Biogas and bio-fuel was utilized into the electric generation or boiler heat in bioenergy-circulation process. The emission of carbon dioxide(CO2) and construction fee of the environmental fundamental facilities related with domestic waste was estimated in the existing city and zero waste clean city, assuming the amount of food waste 35 ton/day, combustible waste 20 ton/day from domestic area. Consequently, 2.7 times lower carbon dioxide emission and 15% construction fee of the environmental fundamental facilities related with domestic waste were obtained from the zero waste clean city by comparing with existing city.

• Korean Chemical Engineering Research
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• v.57 no.6
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• pp.874-882
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• 2019

In this study, the gasification characteristics of four types of unused woody biomass and one waste wood in a lab-scale bubbling fluidized bed gasifier (Diameter: 0.11 m, Height: 0.42 m) were investigated. Effect of equivalence ratio (ER) of 0.15-0.3 and gas velocity of $2.5-5U_0/U_{mf}$ are determined at the constant temperature of $800^{\circ}C$ and fuel feeding rate of 1 kg/h. The silica sand particle having an average particle size of $287{\mu}m$ and olivine with an average particle size of $500{\mu}m$ were used as the bed material, respectively. The average product gas composition of samples is as follows; $H_2$ 3-4 vol.%, CO 15-16 vol.%, $CH_4$ 4 vol.% and $CO_2$ 18-19 vol.% with a lower heating value (LHV) of $1193-1301kcal/Nm^3$ and higher heating value (HHV) of $1262-1377kcal/Nm^3$. In addition, it was found that olivine reduced most of C2 components and increased $H_2$ content compared to silica sand, resulting in cracking reaction of tar. The non-condensable tar decreases by 72% ($1.24{\rightarrow}0.35g/Nm^3$) and the condensable tar decreases by 27% ($4.4{\rightarrow}3.2g/Nm^3$).

• 한국신재생에너지학회:학술대회논문집
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• 2010.11a
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• pp.132.1-132.1
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• 2010

자원고갈과 지구온난화 등으로 재생에너지의 사용 및 보급이 지속적으로 증가할 것으로 예상되지만, 세계적으로 매장량이 풍부한 석탄의 사용량은 2030년 이후에도 지속적으로 증가될 전망이다. 따라서 세계 각국은 기후변화 규제에 대응하면서도 청정하게 석탄을 사용하기 위한 기술의 개발 및 보급을 활발히 진행 중이며, 국내에서도 온실가스 감축과 동시에 국가 성장 동력화를 추진하고 있다. 석탄가스화 기술은 석탄을 가스화하여 생산된 CO, $H_2$가 주성분인 합성가스를 연료로 활용하는 기술로, 이용 효율이 높고 석탄을 천연가스 수준으로 청정하게 사용할 수 있는 차세대 석탄이용 기술이다. 본 연구에서는 pilot급 석탄 가스화기에서 생산된 합성가스에 함유된 산성가스를 고온에서 건식으로 제거하는 시스템을 구축하였으며, 석탄 합성가스를 고온 건식 정제시스템에 공급하기 위한 석탄가스화기의 운전특성을 파악하였다.

• Journal of Environmental Health Sciences
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• v.30 no.5 s.81
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• pp.395-401
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• 2004

In this study, lots of methods have been studing to utilize energy and decrease contaminated effluents. There has been great progress on IGCC (Integrated gasification combined cycle) to reduce thermal energy losses. The following results have been conducted from desulfurization experiments using waste shell to remove $H_{2}S$. Unreacted core model ior desulfuriration rate prediction of sorbent was indicated. These were linear relationship between time and conversion. So co-current diffusion resistance was conducted reaction rate controlling step. The sulfidation rate is likely to be controlled primarily by countercurrent diffusion through the product layer of calcium sulfide(CaS) formed. Maximum desulfurization capacity was observed at 0.631 mm for lime, oyster and hard-shelled mussel. The kinetics of the sorption of $H_{2}S$ by CaO is sensitive to the reaction temperature and particle size at $800^{\circ}C$, and the reaction rate of oyster was faster than the calcined limestone at $700^{\circ}C$.

• 한국연소학회:학술대회논문집
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• 2012.11a
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• pp.71-73
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• 2012

With numerical simulations, this study investigated the combustion and heat transfer of three different coals under air- and oxy-fuel combustion in a 100 MWe boiler. The boiler is retrofitted to an opposed-firing type while maintain the original furnace shape of downshot firing. The boiler achieved good combustion in both combustion modes for three coals tested. However, the contribution of gasification reactions by $CO_2$ and $H_2O$ significantly increased due to the lack of gaseous mixing. This was different from a typical front-wall firing boiler, which showed larger contribution of char oxidation during air-coal combustion. The wall heat flux was lower in oxy-coal mode at a $O_2$ level of 27%, which has to be considered in further development of the process.

• New & Renewable Energy
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• v.3 no.2 s.10
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• pp.47-52
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• 2007

Hydrate phase equilibrium for the binary $CO_{2}$+water and $CH_{4}$+water mixtures in silica gel pore of nominal 6, 30, and 100 nm were measured and compared with the cacluated results based on van der Waals and Platteeuw model. At a specific temperature three-phase hydrate-water-vapor (HLV) equilibrium curves for pore hydrates were shifted to the higher-pressure condition depending on pore sizes when compared with those of bulk hydrates. Notably, hydrate phase equilibria for the case of 100 nominal nm pore size were nearly identical with those of bulk hydrates. The activities of water in porous silica gels were modified to account for capillary effect, and the calculation results were generally in good agreement with the experimental data.

• JOURNAL OF ELECTRICAL WORLD
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• s.452
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• pp.29-34
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• 2014

2014년 5월 한 달 간 우리나라에서 석탄을 이용해 생산한 발전량은 약 1만5,748GW에 달한다. 이는 국내 총 발전량 중 38%에 해당하는 양이다. 특히 유연탄의 경우 kWh당 정산단가가 61.6원에 불과해 원자력(55.4원) 다음으로 경제성이 높은 발전원에 속한다. 그러나 석탄화력의 경우 황산화물, 질소산화물 및 먼지와 지구온난화의 주범으로 꼽히는 온실가스를 배출하고 있어 항상 논란의 대상이 된다. 2011년 기준으로 국내 $CO_2$ 배출량의 약 1/3 정도가 전력분야에서 발생했는데, 이 중 대부분은 석탄화력에서 배출됐다. 즉 환경을 생각하면 비중을 줄여 나가야 하는 것이 맞지만, 경제성 및 효율성을 고려하면 반드시 필요한 발전원이 석탄화력인 셈이다. 이에 비단 우리나라뿐만 아니라 전 세계 전력 산업계에서는 석탄화력의 효율은 높이면서, 온실가스 배출은 줄일 수 있는 기술개발에 적극 나서고 있다. 그 기술 중 가장 현실적이면서 대표적으로 떠오른 분야가 바로 석탄가스화복합발전(Integrated Gasification Combined Cycle, IGCC)이다. 우리나라에서도 IGCC에 대한 관심을 지속적으로 기울여 왔고, 그 노력의 결실로 현재 태안에 국내 최초의 IGCC 실증플랜트를 건설 중에 있다. 현재 IGCC 기술개발은 어느 단계까지 와 있는지, 또 국내외 시장은 얼마나 성장될 것으로 예상되는지 자세히 정리해봤다.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1999.05a
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• pp.17-21
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• 1999

석탄가스화기는 IGCC의 핵심으로서 석탄을 고온에서 열분해 연소 및 가스화하여 연료가스인 저/중열량 가스(CO,H$_2$)로 전환하는 장치이며, Texaco,Destec 및 Shell 등 분류층 가스화기가 발전용으로서 개발중에 있다. 전력연구원에서는 가압분류층 가스화기(Pressured Drop Tube Furnance)를 이용하여 석탄의 가스화 특성을 연구하고 있다. 석탄가스화 공정은 탄종과 운전조건에 따라 그 반응 특성의 편차가 매우 심하고 가스화 특성 실험시 탄종이 자국위주로 되어 있어 우리나라에 많이 수입되는 석탄에 대한 가스화특성에 대한 정보가 많지 않다. 따라서 본 연구는 상용가스화기의 운전조건을 모사한 분위기하에서 석탄가스화 특성을 결정하는 것이 목적이며, Adaro탄을 대상으로 15기압 가압하에서 반응온도 140$0^{\circ}C$, 산소/석탄비 0~l.5, 석탄입자 45~63$mu extrm{m}$, 그리고 석탄 공급율은 6g/min으로 실험조건을 주어 산소/석탄비 변화시 탄소전환율 및 냉가스효율에 대한 석탄가스화 반응 특성을 평가하였다.(중략)

• Journal of the Society of Naval Architects of Korea
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• v.51 no.3
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• pp.220-230
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• 2014

Typical technical issues associated with Floating LNG (FLNG: FSRU and LNG FPSO) design are categorized in terms of global performance evaluation. Although many proven technologies developed through LNG carrier and oil FPSO projects are available for FLNG design, we are still faced with several technical challenges to clear for successful FLNG projects. In this paper, some of the challenges encountered during development of the floating LNG facility (i.e. LNG FPSO and FSRU) will be reviewed together with their investigated solution. At the same time, research of design improvement including new LNG-related technologies such as combined containment system will be presented to overcome the unrevealed challenges for the FLNG development.

• KEPCO Journal on Electric Power and Energy
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• v.3 no.2
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• pp.141-146
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• 2017

In this work, a simulation study on net 500 MW class of Poly-Generation was conducted for the retrofit of an aged natural gas combined cycle. An entrained gasifier which has a capacity of maximum $260,000Nm^3/h$, 50 MW class of a Polymer Electrolyte Membrane Fuel Cell, and H-class Gas Turbine were selected as key processes. After unit design for those employed processes was set up and combined, the simulation was carried out with Gate-Cycle software (Ver. 6.0) for two cases. The selected cases are a retrofit type (Poly-Gen 1) and a new type (Poly-Gen 2). It was found that the efficiency of the retrofit case is 2.7% lower than that of the new case.